TW202035316A - Opaque quartz glass and production method therefor - Google Patents

Opaque quartz glass and production method therefor Download PDF

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TW202035316A
TW202035316A TW108144304A TW108144304A TW202035316A TW 202035316 A TW202035316 A TW 202035316A TW 108144304 A TW108144304 A TW 108144304A TW 108144304 A TW108144304 A TW 108144304A TW 202035316 A TW202035316 A TW 202035316A
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quartz glass
opaque quartz
slurry
silicon nitride
particle size
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TW108144304A
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Chinese (zh)
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伊藤千絵美
武藤健
佐藤政
鈴木孝哉
国吉実
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日商東曹石英有限公司
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    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/08Other methods of shaping glass by foaming
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B20/00Processes specially adapted for the production of quartz or fused silica articles, not otherwise provided for
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C11/00Multi-cellular glass ; Porous or hollow glass or glass particles

Abstract

The objective of the invention is to provide an opaque quartz glass having excellent heat ray blocking properties, mechanical strength, and surface smoothness. As a result of using, as a foaming agent, silicon nitride generated by the abrasion of silicon nitride beads which have a mean particle size of 0.1 mm to 3 mm and are used as a grinding medium when wet grinding a slurry comprising 45 to 75% by weight of silica powder dispersed in water, the opaque quartz glass contains air bubbles with a mean particle size of 2 to 30 [mu]m that are shaped as independent sphere shapes having a mean roundness of 0.8 or greater, and has a density of 1.90 to 2.20 g/cm3, a whiteness of 80% or higher and/or a reflectivity of 80% or higher at a thickness of 3 mm for light of 0.2 to 3 [mu]m wavelength, a three-point bending strength of 80 MPa or greater, a surface roughness Ra of 0.7 [mu]m or less for the firing finish surface, and excellent heat ray blocking properties, mechanical strength, and surface smoothness.

Description

不透明石英玻璃及其製造方法Opaque quartz glass and its manufacturing method

本發明係關於一種熱線阻斷性、機械強度、表面平滑性優異之不透明石英玻璃及其製造方法。 更詳細而言,係關於一種可適宜用於半導體製造裝置用構件、光學機器之零件等之不透明石英玻璃及其製造方法。The present invention relates to an opaque quartz glass with excellent hot wire blocking properties, mechanical strength, and surface smoothness, and a manufacturing method thereof. In more detail, it relates to an opaque quartz glass suitable for use in components for semiconductor manufacturing devices, parts of optical equipment, and the like, and a method of manufacturing the same.

石英玻璃因透光性、耐熱性、耐化學品性優異,故用於照明機器、光學機器零件、半導體工業用構件、物理化學機器等各種用途。其中,石英玻璃中含有氣泡之不透明石英玻璃因其優異之熱線阻斷性而被用於半導體熱處理裝置之凸緣或爐心管。又,因遮光性優異,故亦用作投影機用光源燈之反射器基材等光學機器零件。Quartz glass has excellent light transmittance, heat resistance, and chemical resistance, so it is used in various applications such as lighting equipment, optical equipment parts, semiconductor industrial components, and physical and chemical equipment. Among them, the opaque quartz glass containing bubbles in the quartz glass is used for the flange or the furnace core tube of the semiconductor heat treatment device because of its excellent heat resistance. In addition, because of its excellent light-shielding properties, it is also used as a reflector base material for light source lamps for projectors and other optical equipment parts.

以往,作為不透明石英玻璃之製造方法,已知如下方法(例如參照專利文獻1)等,即,藉由乾式混合向結晶質二氧化矽或非晶質二氧化矽中添加氮化矽等發泡劑,利用氫氧焰進行加熱熔融。然而,該製造方法及製造之不透明石英玻璃存在如下課題。 (1)由於在加熱熔融時發泡劑散失,故為了獲得實用之不透明度,需要添加大量之發泡劑,耗費成本。 (2)由於未均勻地混合而凝聚之發泡劑會氣化形成氣泡,故氣泡變大,不透明石英玻璃之機械強度或光之反射率降低。 (3)由於氣泡較大,故燒製完成面粗糙,形成凹凸面,於使用不透明石英玻璃作為凸緣之情形時,與裝置之密接性變差,成為洩漏之原因。又,於用作反射器基材之情形時,存在燈光洩漏,對投影機內部之電子零件產生不良影響之情形。In the past, as a method for producing opaque quartz glass, the following method (for example, refer to Patent Document 1), etc., is known by dry mixing by adding silicon nitride or the like to crystalline silicon dioxide or amorphous silicon dioxide. The agent is heated and melted with a hydrogen-oxygen flame. However, the manufacturing method and the manufactured opaque quartz glass have the following problems. (1) Since the blowing agent is lost during heating and melting, in order to obtain practical opacity, a large amount of blowing agent needs to be added, which is costly. (2) The foaming agent that is not uniformly mixed and condensed will vaporize to form bubbles, so the bubbles become larger, and the mechanical strength or light reflectivity of the opaque quartz glass decreases. (3) Due to the large air bubbles, the firing surface is rough, forming an uneven surface. When opaque quartz glass is used as a flange, the adhesion to the device becomes poor, which causes leakage. In addition, when used as a reflector substrate, there is a situation where the light leaks, which adversely affects the electronic components inside the projector.

另一方面,亦提出如下方法(例如參照專利文獻2),即,不添加發泡劑,對非晶質二氧化矽粉末之成型體以其熔融溫度以下之溫度進行加熱,於完全緻密化之前中斷熱處理,而部分性地燒結。藉由該製造方法製造之不透明石英玻璃能夠縮小氣泡之平均粒徑,但存在如下問題,即,若燒結至氣泡變成密閉氣泡為止,則氣泡之含有密度變小,紅外線之反射率降低;或由於氣泡為非球狀,故應力集中於氣泡端部,機械強度降低。 [先前技術文獻] [專利文獻]On the other hand, the following method is also proposed (for example, refer to Patent Document 2), that is, without adding a foaming agent, the molded body of amorphous silica powder is heated at a temperature below its melting temperature, before being completely densified Interrupt the heat treatment and partially sinter. The opaque quartz glass manufactured by this manufacturing method can reduce the average particle size of the bubbles, but it has the following problems. That is, if sintered until the bubbles become closed bubbles, the density of the bubbles decreases and the reflectivity of infrared rays decreases; or The bubble is non-spherical, so the stress is concentrated at the end of the bubble, and the mechanical strength is reduced. [Prior Technical Literature] [Patent Literature]

[專利文獻1]日本專利第3043032號公報 [專利文獻2]日本專利第3394323號公報[Patent Document 1] Japanese Patent No. 3043032 [Patent Document 2] Japanese Patent No. 3394323

[發明所欲解決之課題][The problem to be solved by the invention]

本發明之課題在於為了解決上述課題而提供一種熱線阻斷性、機械強度、表面平滑性優異之不透明石英玻璃及其製造方法。 [解決課題之技術手段]The subject of the present invention is to provide an opaque quartz glass with excellent heat-ray blocking properties, mechanical strength, and surface smoothness, and a method of manufacturing the same, in order to solve the above-mentioned problems. [Technical means to solve the problem]

本發明人等發現,對使二氧化矽粉末分散於水中而成之漿料進行濕式粉碎時,藉由使用氮化矽珠粒作為粉碎介質,將由氮化矽珠粒之磨耗所產生之氮化矽粉末作為發泡劑添加至漿料中,對將該漿料進行噴霧乾燥造粒而成之熔融原料進行加熱熔融,藉此使氣泡之形狀為獨立球狀,平均粒徑為2~30 μm,切割面中之氣泡之平均正圓度為0.8以上,藉此,可獲得熱線阻斷性及機械強度優異,燒製完成面之平滑性良好之不透明石英玻璃,從而完成了本發明。 (1)關於氣泡之平均粒徑,對試樣進行切割,藉由桌上型掃描式電子顯微鏡(日立製作所TM4000Plus)觀察20個以上氣泡之形狀,對其圖像進行處理,測定各氣泡之面積A,代入下述式1求出值D,將該值D之平均值設為平均粒徑。 (2)關於氣泡之平均正圓度,對試樣進行切割,藉由桌上型掃描式電子顯微鏡(日立製作所TM4000Plus)觀察20個以上氣泡之形狀,對其圖像進行處理,測定各氣泡之面積A及外周L,代入式2求出值S,將該值S之平均值設為平均正圓度。

Figure 02_image001
π為圓周率The inventors of the present invention found that when wet pulverizing a slurry formed by dispersing silicon dioxide powder in water, by using silicon nitride beads as a pulverizing medium, the nitrogen generated by the abrasion of the silicon nitride beads Silica powder is added to the slurry as a foaming agent, and the molten raw material obtained by spray drying and granulating the slurry is heated and melted, thereby making the shape of the bubbles into independent spheres with an average particle size of 2-30 μm, the average roundness of the bubbles in the cut surface is 0.8 or more, by which it is possible to obtain an opaque quartz glass with excellent hot-line blocking and mechanical strength, and good smoothness of the fired surface, thereby completing the present invention. (1) Regarding the average particle size of bubbles, cut the sample, observe the shape of more than 20 bubbles with a desktop scanning electron microscope (Hitachi, Ltd. TM4000Plus), process the images, and measure the area of each bubble A, the value D is obtained by substituting the following formula 1 and the average value of the value D is defined as the average particle diameter. (2) Regarding the average roundness of the bubbles, cut the sample, observe the shape of more than 20 bubbles with a desktop scanning electron microscope (Hitachi, Ltd. TM4000Plus), process the images, and measure the size of each bubble The area A and the outer circumference L are substituted into Equation 2 to obtain the value S, and the average value of the value S is set as the average roundness.
Figure 02_image001
π is the ratio of pi

關於本發明之不透明石英玻璃,氣泡為球形,平均粒徑為2~30 μm,理想的是平均氣泡徑為5~25 μm,更理想的是8~10 μm。若平均氣泡徑小於2 μm,則光之散射變弱。另一方面,若平均氣泡徑大於30 μm,則同樣地光之散射變弱,且石英玻璃表面之凹凸變大,表面之平滑性及密封性變差。Regarding the opaque quartz glass of the present invention, the bubbles are spherical and have an average particle size of 2-30 μm. The average bubble diameter is preferably 5-25 μm, and more preferably 8-10 μm. If the average bubble diameter is less than 2 μm, the light scattering becomes weaker. On the other hand, if the average bubble diameter is greater than 30 μm, the scattering of light is similarly weak, and the unevenness of the quartz glass surface becomes larger, and the smoothness and sealing of the surface deteriorate.

本發明之不透明石英玻璃之氣泡為獨立球狀。於氣泡形狀為非球狀之情形時,應力集中於氣泡端部,因此獲得之不透明石英玻璃之機械強度降低。 關於氣泡之球狀程度,分別測定藉由掃描式電子顯微鏡觀察不透明石英玻璃之剖面時之氣泡之正圓度,其平均值較佳為大於0.8,更佳為0.9以上。正圓度越小,應力越容易集中於氣泡端部,機械強度越降低,因此欠佳。 關於平均正圓度,對試樣進行切割後,藉由桌上型掃描式電子顯微鏡(日立TM4000Plus)觀察20個以上氣泡之形狀,對其圖像進行處理,測定各氣泡之面積A及外周L,代入上述式2求出值S,將其進行平均而設為平均正圓度。 本發明之不透明石英玻璃之白度為80以上。關於白度,將使用色彩色差計(Konica Minolta公司製造之CR-400)依據JIS Z 8722測定之亮度設為白度。若白度未達80,則熱線阻斷性降低,絕熱性降低。 本發明之不透明石英玻璃之於玻璃厚3 mm之波長0.2~3 μm之光之反射率為80%以上。若反射率未達80%,則與亮度同樣地熱線阻斷性降低,絕熱性降低。The bubbles of the opaque quartz glass of the present invention are independent spheres. When the bubble shape is aspherical, the stress is concentrated at the end of the bubble, so the mechanical strength of the obtained opaque quartz glass is reduced. Regarding the spherical degree of the bubbles, the roundness of the bubbles when observing the cross-section of the opaque quartz glass by a scanning electron microscope is measured, and the average value is preferably greater than 0.8, more preferably 0.9 or greater. The smaller the roundness, the easier the stress is concentrated on the end of the bubble, and the lower the mechanical strength, so it is not good. Regarding the average roundness, after cutting the sample, observe the shape of more than 20 bubbles with a desktop scanning electron microscope (Hitachi TM4000Plus), process the image, and measure the area A and outer circumference L of each bubble , Substitute the above-mentioned formula 2 to obtain the value S, and average it to set the average roundness. The whiteness of the opaque quartz glass of the present invention is 80 or more. Regarding the whiteness, the brightness measured in accordance with JIS Z 8722 using a color difference meter (CR-400 manufactured by Konica Minolta) is defined as the whiteness. If the whiteness is less than 80, the heat-blocking properties are reduced, and the thermal insulation properties are reduced. The reflectance of the opaque quartz glass of the present invention to light with a glass thickness of 3 mm and a wavelength of 0.2-3 μm is above 80%. If the reflectance is less than 80%, the heat-ray barrier properties will decrease like the brightness, and the heat insulation properties will decrease.

本發明之不透明石英玻璃之密度為1.90~2.20 g/cm3 。若密度未達1.90 g/cm3 ,則機械強度降低。若超過2.20 g/cm3 ,則氣泡之含量減少,光之散射變弱,熱線阻斷性降低。 本發明之不透明石英玻璃之3點彎曲強度為80 MPa以上。若3點彎曲強度未達80 MPa,則例如用於半導體製造裝置之凸緣或爐心管時之破損之虞變大。The density of the opaque quartz glass of the present invention is 1.90-2.20 g/cm 3 . If the density is less than 1.90 g/cm 3 , the mechanical strength will decrease. If it exceeds 2.20 g/cm 3 , the content of bubbles will decrease, the scattering of light will become weaker, and the heat ray blocking performance will decrease. The three-point bending strength of the opaque quartz glass of the present invention is 80 MPa or more. If the three-point bending strength is less than 80 MPa, for example, the flange or furnace tube of a semiconductor manufacturing device may be damaged.

本發明之不透明石英玻璃之燒製完成面之表面粗糙度Ra為0.7 μm以下,進而較佳為0.6 μm以下。若燒製完成面之表面粗糙度Ra超過0.7 μm,則與裝置之接著面之密接性變差,例如用於凸緣時,成為洩漏之原因,故欠佳。又,於用作投影機用光源燈之反射器基材時,燈光洩漏,對投影機內部之電子零件產生不良影響。The surface roughness Ra of the fired surface of the opaque quartz glass of the present invention is 0.7 μm or less, and more preferably 0.6 μm or less. If the surface roughness Ra of the fired surface exceeds 0.7 μm, the adhesion to the bonding surface of the device becomes poor. For example, when it is used in a flange, it becomes a cause of leakage, so it is not good. In addition, when used as a reflector base material for a light source lamp for a projector, the light leaks, which adversely affects the electronic components inside the projector.

其次,對本發明之製造方法進行說明。 本發明之製造方法之特徵在於,對使二氧化矽粉末分散於水中而成之漿料進行濕式粉碎時,使用氮化矽珠粒作為粉碎介質,使用由氮化矽珠粒之磨耗所產生之氮化矽作為發泡劑。進而,其特徵在於將對該漿料進行噴霧乾燥造粒而成之造粒粉設為熔融原料。Next, the manufacturing method of the present invention will be explained. The manufacturing method of the present invention is characterized in that when the slurry formed by dispersing silicon dioxide powder in water is wet crushed, silicon nitride beads are used as the crushing medium, and the abrasion of silicon nitride beads is used. The silicon nitride is used as a blowing agent. Furthermore, it is characterized in that granulated powder obtained by spray drying and granulating the slurry is used as a molten raw material.

以下,針對每個步驟加以詳細說明。再者,對所有步驟而言,為了於步驟中不產生雜質污染,必須充分地選定所使用之裝置等。 (1)原料粉末之選定 關於二氧化矽粉末,其製法並無特別限定,例如可使用利用矽烷氧化物之水解而製造之非晶質二氧化矽粉末或利用氫氧焰等使四氯化矽水解而製作之二氧化矽粉末等。又,亦可使用將天然水晶粉碎而成之粉末或氣相二氧化矽(fumed silica)。 二氧化矽粉末之平均粒徑較佳為300 μm以下。若平均粒徑超過300 μm而過大,則二氧化矽粉末之濕式粉碎耗費較長時間,因此會導致生產性降低或生產成本增大,故欠佳。 二氧化矽粉末之平均粒徑使用雷射繞射粒度分佈測定裝置(Malvern公司製造之Mastersizer3000)進行測定。 (2)漿料之調整 使二氧化矽粉末分散於水中而成之漿料之濃度為45~75 wt%,理想的是60~70 wt%。若超過75 wt%,則漿料之黏度變高,無法進行濕式粉碎。若未達45 wt%之濃度,則水分量較多,乾燥時需要之熱量變多,導致生產性降低或生產成本增大,故不理想。 (3)發泡劑之添加 發泡劑使用由氮化矽珠粒之磨耗所產生之氮化矽。氮化矽珠粒之平均粒徑較佳為0.1~3 mm。若氮化矽珠粒之平均粒徑大於3 mm,則珠粒之接觸面積減少,因此珠粒之磨耗量降低,發泡劑之添加耗費較長時間。另一方面,若珠粒平均粒徑小於0.1 mm,則珠粒之接觸面積增大,因此珠粒之磨耗量增加,難以控制發泡劑添加量。 作為磨耗氮化矽珠粒之裝置,使用珠磨機、球磨機、振動磨機、磨碎機(attritor)之任一者。尤其理想的是使用珠磨機。 發泡劑之氮化矽相對於二氧化矽粉末之添加量為0.1~100 ppm,理想的是1~50 ppm。若氮化矽之添加量未達0.1 ppm,則氮化矽之供給量不充分,白色化、不透明化不充分,又,若超過100 ppm,則氣泡彼此結合,氣泡徑變大,因此白度降低。 發泡劑相對於二氧化矽粉末之添加量可藉由改變使用氮化矽珠粒之二氧化矽粉末之粉碎時間而調整為0.1~100 ppm。又,亦可於製作發泡劑之濃度200~10000 ppm之漿料後,利用不含發泡劑之漿料進行稀釋,將發泡劑之添加量調整為0.1~500 ppm。 (4)添加發泡劑之漿料之濕式粉碎 其次,對於調整了發泡劑之濃度之漿料,使用除氮化矽珠粒以外之平均粒徑0.1 mm~3 mm之選自石英玻璃珠粒、氧化鋯珠粒、碳化矽珠粒、氧化鋁珠粒中之1種或複數種珠粒,進一步進行濕式粉碎,直至漿料中所含之固形物之BET比表面積成為2 m2 /g以上。理想的是進行濕式粉碎直至成為4 m2 /g以上、更理想的是成為6 m2 /g以上。若BET比表面積小於2 m2 /g,則造粒粉之強度降低,造粒崩散,氫氧焰熔融時之良率降低。 漿料之濕式粉碎之方法並無特別限定,濕式粉碎之方法可例示珠磨機粉碎、球磨機粉碎、振動磨機粉碎、磨碎機粉碎等。尤其理想的是珠磨機粉碎。 (5)噴霧乾燥造粒 其次,對藉由上述方法製作之漿料進行噴霧乾燥,獲得造粒粉。所獲得之造粒粉實質上為球形,平均粒徑為30~200 μm,含水率為3 wt%以下。若平均粒徑未達30 μm,則於氫氧焰熔融時造粒粉會散逸,良率變差。若平均粒徑超過200 μm,則造粒崩散,於氫氧焰熔融時散逸,良率變差。若含水率超過3 wt%,則造粒粉之流動性變差,氫氧焰熔融時之造粒粉之每單位時間之供給量減少,因此生產性變差。 造粒粉之平均粒徑與二氧化矽粉末同樣使用Malvern公司製造之雷射繞射粒度分佈測定裝置(Mastersizer3000)進行測定。 (6)造粒粉之熔融 其次,利用氫氧焰使獲得之造粒粉熔融,或者於真空環境下進行加熱熔融,藉此可獲得本發明之不透明石英玻璃。利用氫氧焰之熔融係藉由氧與氫之反應而產生水,因此不透明石英玻璃之OH基濃度成為100~1000 ppm,成為高於在真空環境下熔融者之值。真空環境下之熔融不產生水,因此OH基濃度為10 ppm以下,成為低於利用氫氧焰熔融者之值。 利用製造石英構件時使用之帶鋸、線鋸、取心鑽等加工機對經過上述步驟所獲得之不透明石英玻璃之錠進行加工,藉此,可獲得符合用途之形狀之不透明石英玻璃構件。 (7)不透明石英玻璃之純度 不透明石英玻璃之純度可根據原料中使用之二氧化矽粉末之種類進行調整。除用於粉碎介質之珠粒之構成元素以外,與原料二氧化矽粉末大致相同。 [發明之效果]Hereinafter, each step is explained in detail. Furthermore, for all the steps, in order not to cause contamination by impurities in the steps, it is necessary to fully select the equipment to be used. (1) Selection of raw material powder Regarding the silicon dioxide powder, the preparation method is not particularly limited. For example, amorphous silicon dioxide powder produced by the hydrolysis of silanoxide can be used, or silicon tetrachloride can be made by hydrogen oxygen flame. Silicon dioxide powder produced by hydrolysis. In addition, powder or fumed silica obtained by crushing natural crystal can also be used. The average particle size of the silicon dioxide powder is preferably 300 μm or less. If the average particle size exceeds 300 μm and is too large, the wet pulverization of the silicon dioxide powder will take a long time, which will result in a decrease in productivity or an increase in production cost, which is not preferable. The average particle size of the silicon dioxide powder is measured using a laser diffraction particle size distribution measuring device (Mastersizer 3000 manufactured by Malvern). (2) Adjustment of slurry The concentration of slurry made by dispersing silica powder in water is 45-75 wt%, ideally 60-70 wt%. If it exceeds 75 wt%, the viscosity of the slurry becomes high and wet pulverization cannot be performed. If the concentration is less than 45 wt%, the water content will be large, and the heat required for drying will increase, resulting in reduced productivity or increased production costs, which is not ideal. (3) Addition of blowing agent The blowing agent uses silicon nitride produced by the abrasion of silicon nitride beads. The average particle diameter of the silicon nitride beads is preferably 0.1-3 mm. If the average particle size of the silicon nitride beads is greater than 3 mm, the contact area of the beads is reduced, so the wear of the beads is reduced, and the addition of the blowing agent takes a long time. On the other hand, if the average particle diameter of the beads is less than 0.1 mm, the contact area of the beads will increase, so the wear of the beads will increase, making it difficult to control the amount of blowing agent added. As a device for abrading silicon nitride beads, any one of a bead mill, a ball mill, a vibration mill, and an attritor is used. It is especially desirable to use a bead mill. The amount of silicon nitride of the blowing agent relative to the silicon dioxide powder is 0.1-100 ppm, ideally 1-50 ppm. If the addition amount of silicon nitride is less than 0.1 ppm, the supply amount of silicon nitride is insufficient, and the whitening and opacity are insufficient. If it exceeds 100 ppm, the bubbles will be combined with each other and the bubble diameter will increase, resulting in whiteness reduce. The amount of blowing agent added to the silicon dioxide powder can be adjusted to 0.1-100 ppm by changing the pulverization time of the silicon dioxide powder using silicon nitride beads. In addition, after making a slurry with a foaming agent concentration of 200-10000 ppm, it can be diluted with a slurry without a foaming agent to adjust the addition amount of the foaming agent to 0.1-500 ppm. (4) Wet pulverization of the slurry with foaming agent. Secondly, for the slurry with the concentration of the foaming agent adjusted, use silica glass with an average particle size of 0.1 mm~3 mm except for silicon nitride beads. One or more of beads, zirconia beads, silicon carbide beads, and alumina beads are further wet crushed until the BET specific surface area of the solids contained in the slurry becomes 2 m 2 /g above. It is desirable to perform wet grinding until it becomes 4 m 2 /g or more, more desirably 6 m 2 /g or more. If the BET specific surface area is less than 2 m 2 /g, the strength of the granulated powder will decrease, the granulation will collapse, and the yield rate during the melting of the hydrogen-oxygen flame will decrease. The method of wet pulverization of the slurry is not particularly limited, and the method of wet pulverization can be exemplified by bead mill pulverization, ball mill pulverization, vibration mill pulverization, and grinder pulverization. Especially ideal is bead mill pulverization. (5) Spray drying and granulation Next, the slurry produced by the above method is spray-dried to obtain granulated powder. The obtained granulated powder is substantially spherical, with an average particle size of 30-200 μm, and a moisture content of 3 wt% or less. If the average particle size is less than 30 μm, the granulated powder will dissipate when the oxyhydrogen flame is melted, resulting in poor yield. If the average particle size exceeds 200 μm, the granulation will collapse and dissipate when the oxyhydrogen flame is melted, resulting in poor yield. If the water content exceeds 3 wt%, the fluidity of the granulated powder will deteriorate, and the supply amount of the granulated powder per unit time during the oxyhydrogen flame melting will decrease, resulting in poor productivity. The average particle size of the granulated powder is measured using the laser diffraction particle size distribution measuring device (Mastersizer 3000) manufactured by Malvern Company in the same way as the silica powder. (6) Melting of the granulated powder Next, the obtained granulated powder is melted by a hydrogen-oxygen flame, or heated and melted in a vacuum environment, thereby obtaining the opaque quartz glass of the present invention. The fusion using the oxyhydrogen flame produces water by the reaction of oxygen and hydrogen. Therefore, the OH group concentration of opaque quartz glass becomes 100-1000 ppm, which is higher than that of melting in a vacuum environment. Melting in a vacuum environment does not produce water, so the OH group concentration is 10 ppm or less, which is lower than the value of melting with a hydrogen-oxygen flame. The ingots of opaque quartz glass obtained through the above steps are processed by processing machines such as band saws, wire saws, and core drills used in the manufacture of quartz components, thereby obtaining opaque quartz glass components with shapes suitable for the purpose. (7) The purity of opaque quartz glass The purity of opaque quartz glass can be adjusted according to the type of silicon dioxide powder used in the raw material. Except for the constituent elements of the beads used for the crushing medium, it is roughly the same as the raw material silicon dioxide powder. [Effects of Invention]

本發明之不透明石英玻璃之熱線阻斷性、機械強度、表面平滑性及密封性優異,可適宜用作尤其是於半導體製造領域中使用之各種爐心管、治具類及鐘罩等容器類,例如矽晶圓處理用爐心管或其凸緣部、絕熱片、矽熔融用坩堝等之構成材料。又,作為光學機器零件亦可用於投影機用光源燈之反射器基材。 進而,根據本發明之不透明石英玻璃之製造方法,可獲得熱線阻斷性、機械強度、表面平滑性及密封性優異之不透明石英玻璃。The opaque quartz glass of the present invention is excellent in heat resistance, mechanical strength, surface smoothness and sealing, and can be suitably used as various furnace tubes, fixtures, bell jars and other containers used in the semiconductor manufacturing field. , Such as the core tube for silicon wafer processing or its flange, heat insulation sheet, crucible for silicon melting, etc. In addition, it can also be used as a reflector substrate of a light source lamp for a projector as an optical device component. Furthermore, according to the manufacturing method of the opaque quartz glass of the present invention, an opaque quartz glass with excellent heat ray blocking properties, mechanical strength, surface smoothness, and sealing properties can be obtained.

<實施例> 以下,利用實施例具體地說明本發明,但本發明並不限定於實施例。<Example> Hereinafter, the present invention will be specifically explained using examples, but the present invention is not limited to the examples.

(實施例1) 使用非晶質二氧化矽(D10 :38 μm,D50 :67 μm,D90 :110 μm)作為二氧化矽原料粉末。使非晶質二氧化矽分散於水中,製成漿料,將濃度調整為67 wt%。其次,將經調整之漿料投入至珠磨機粉碎機,使用平均粒徑2.0 mm之氮化矽珠粒,進行濕式粉碎直至氮化矽相對於漿料中之二氧化矽粉末之濃度成為250 ppm,製備漿料(A)。另一方面,利用不含發泡劑之二氧化矽原料粉末製備固形物濃度為67 wt%之漿料B。其後,利用漿料(B)以氮化矽相對於漿料中之二氧化矽粉末之濃度成為1 ppm之方式將漿料(A)加以稀釋,製備粉碎造粒用漿料。使用平均粒徑2.0 mm之氧化鋯珠粒對粉碎造粒用漿料進行濕式粉碎,直至BET比表面積成為6.0 m2 /g。(Example 1) Amorphous silicon dioxide (D 10 : 38 μm, D 50 : 67 μm, D 90 : 110 μm) was used as the silicon dioxide raw material powder. Disperse amorphous silicon dioxide in water to prepare a slurry, and adjust the concentration to 67 wt%. Next, put the adjusted slurry into the bead mill and use silicon nitride beads with an average particle size of 2.0 mm to perform wet pulverization until the concentration of silicon nitride relative to the silicon dioxide powder in the slurry becomes 250 ppm, prepare slurry (A). On the other hand, slurry B with a solid content concentration of 67 wt% was prepared using silica raw material powder without foaming agent. After that, the slurry (A) was diluted with the slurry (B) so that the concentration of silicon nitride relative to the silicon dioxide powder in the slurry became 1 ppm to prepare a slurry for crushing and granulation. Using zirconia beads with an average particle diameter of 2.0 mm, the slurry for crushing and granulation was wet crushed until the BET specific surface area became 6.0 m 2 /g.

其次,對利用上述方法製作之粉碎造粒用漿料進行噴霧乾燥,獲得造粒粉。關於所獲得之造粒粉,其平均粒徑為80 μm,含水率為1 wt%。利用氫氧焰使獲得之造粒粉熔融,製造柱狀不透明石英玻璃錠。 關於獲得之柱狀不透明石英玻璃錠之氣泡,目視觀察時,均勻地分散,美觀方面亦優異。Next, the slurry for crushing and granulation produced by the above method is spray-dried to obtain granulated powder. Regarding the obtained granulated powder, the average particle size was 80 μm and the moisture content was 1 wt%. The obtained granulated powder is melted by a hydrogen-oxygen flame to produce a cylindrical opaque quartz glass ingot. With regard to the bubbles of the obtained columnar opaque quartz glass ingot, when visually observed, the bubbles were uniformly dispersed, and the appearance was also excellent.

(實施例2) 除了將氮化矽之添加量設為5 ppm以外,依據實施例1製造柱狀不透明石英玻璃錠。 關於獲得之柱狀不透明石英玻璃錠之氣泡,目視觀察時,均勻地分散,美觀方面亦優異。(Example 2) Except that the addition amount of silicon nitride was set to 5 ppm, a columnar opaque quartz glass ingot was manufactured according to Example 1. With regard to the bubbles of the obtained columnar opaque quartz glass ingot, when visually observed, the bubbles were uniformly dispersed, and the appearance was also excellent.

(實施例3) 除了將氮化矽之添加量設為0.3 ppm以外,依據實施例1製造柱狀不透明石英玻璃錠。 關於獲得之柱狀不透明石英玻璃錠之氣泡,目視觀察時,均勻地分散,美觀方面亦優異。(Example 3) Except that the addition amount of silicon nitride was set to 0.3 ppm, a columnar opaque quartz glass ingot was manufactured according to Example 1. With regard to the bubbles of the obtained columnar opaque quartz glass ingot, when visually observed, the bubbles were uniformly dispersed, and the appearance was also excellent.

(實施例4) 與實施例1同樣使作為二氧化矽原料粉末之非晶質二氧化矽分散於水中,將其濃度調整為50 wt%。其次,將經調整之漿料投入至珠磨機粉碎機,使用平均粒徑0.3 mm之氮化矽珠粒進行濕式粉碎,直至漿料中之氮化矽濃度成為1 ppm。其後,去除氮化矽珠粒,使用平均粒徑0.3 mm之氧化鋯珠粒對添加有發泡劑之漿料進行濕式粉碎,直至BET比表面積成為3.0 m2 /g。其次,對利用上述方法製作之漿料進行乾燥噴霧,獲得造粒粉。關於獲得之造粒粉,其平均粒徑為40 μm,含水率為1 wt%。利用氫氧焰使獲得之造粒粉熔融,製造柱狀不透明石英玻璃錠。 關於獲得之柱狀不透明石英玻璃錠之氣泡,目視觀察時,均勻地分散,美觀方面亦優異。(Example 4) In the same manner as in Example 1, amorphous silica as the raw material powder of silica was dispersed in water, and the concentration was adjusted to 50 wt%. Next, put the adjusted slurry into the bead mill and use silicon nitride beads with an average particle size of 0.3 mm to perform wet pulverization until the concentration of silicon nitride in the slurry becomes 1 ppm. After that, the silicon nitride beads were removed, and the zirconia beads with an average particle size of 0.3 mm were used to wet pulverize the slurry added with the foaming agent until the BET specific surface area became 3.0 m 2 /g. Next, the slurry prepared by the above method is dried and sprayed to obtain granulated powder. Regarding the obtained granulated powder, the average particle size was 40 μm and the moisture content was 1 wt%. The obtained granulated powder is melted by a hydrogen-oxygen flame to produce a columnar opaque quartz glass ingot. With regard to the bubbles of the obtained columnar opaque quartz glass ingot, when visually observed, the bubbles were uniformly dispersed, and the appearance was also excellent.

(實施例5) 使與實施例1相同之作為二氧化矽原料粉末之非晶質二氧化矽分散於水中,將其濃度調整為70 wt%。其次,將經調整之漿料投入至珠磨機粉碎機,使用平均粒徑1.0 mm之氮化矽珠粒進行濕式粉碎,直至漿料中之氮化矽濃度成為1 ppm。其後,去除氮化矽珠粒,使用平均粒徑1.0 mm之氧化鋯珠粒對添加有發泡劑之漿料進行濕式粉碎,直至BET比表面積成為8.0 m2 /g。其次,對利用上述方法製作之漿料進行乾燥噴霧,獲得造粒粉。關於獲得之造粒粉,其平均粒徑為150 μm,含水率為1 wt%。利用氫氧焰使獲得之造粒粉熔融,製造柱狀不透明石英玻璃錠。 關於獲得之柱狀不透明石英玻璃錠之氣泡,目視觀察時,均勻地分散,美觀方面亦優異。(Example 5) The same amorphous silicon dioxide as the silicon dioxide raw material powder as in Example 1 was dispersed in water, and its concentration was adjusted to 70 wt%. Secondly, put the adjusted slurry into a bead mill and use silicon nitride beads with an average particle size of 1.0 mm for wet pulverization until the concentration of silicon nitride in the slurry becomes 1 ppm. After that, the silicon nitride beads were removed, and the zirconia beads with an average particle size of 1.0 mm were used to wet pulverize the slurry added with the foaming agent until the BET specific surface area became 8.0 m 2 /g. Next, the slurry prepared by the above method is dried and sprayed to obtain granulated powder. Regarding the obtained granulated powder, its average particle size was 150 μm and the moisture content was 1 wt%. The obtained granulated powder is melted by a hydrogen-oxygen flame to produce a columnar opaque quartz glass ingot. With regard to the bubbles of the obtained columnar opaque quartz glass ingot, when visually observed, the bubbles were uniformly dispersed, and the appearance was also excellent.

(實施例6) 使用非晶質二氧化矽(D10 :38 μm,D50 :67 μm,D90 :110 μm)作為二氧化矽原料粉末。使非晶質二氧化矽分散於水中,製成漿料,將濃度調整為67 wt%。其次,將經調整之漿料投入至珠磨機粉碎機,使用平均粒徑2.0 mm之氮化矽珠粒進行濕式粉碎,直至氮化矽相對於漿料中之二氧化矽粉末之濃度成為250 ppm,製備漿料(A)。另一方面,利用不含發泡劑之二氧化矽原料粉末製備固形物濃度為67 wt%之漿料B。其後,利用漿料(B)以氮化矽相對於漿料中之二氧化矽粉末之濃度成為1 ppm之方式將漿料(A)加以稀釋,製備粉碎造粒用漿料。使用平均粒徑2.0 mm之氧化鋯珠粒對粉碎造粒用漿料進行濕式粉碎,直至BET比表面積成為6.0 m2 /g。其次,對利用上述方法製作之粉碎造粒用漿料進行噴霧乾燥,獲得造粒粉。關於獲得之造粒粉,其平均粒徑為80 μm,含水率為1 wt%。利用氫氧焰使獲得之造粒粉熔融,製造板塊(slab)狀不透明石英玻璃錠。 關於獲得之板塊狀不透明石英玻璃錠之氣泡,目視觀察時,均勻地分散,美觀方面亦優異。(Example 6) Amorphous silicon dioxide (D 10 : 38 μm, D 50 : 67 μm, D 90 : 110 μm) was used as the silicon dioxide raw material powder. Disperse amorphous silicon dioxide in water to prepare a slurry, and adjust the concentration to 67 wt%. Next, put the adjusted slurry into the bead mill and use silicon nitride beads with an average particle size of 2.0 mm to perform wet pulverization until the concentration of silicon nitride relative to the silicon dioxide powder in the slurry becomes 250 ppm, prepare slurry (A). On the other hand, slurry B with a solid content concentration of 67 wt% was prepared using silica raw material powder without foaming agent. After that, the slurry (A) was diluted with the slurry (B) so that the concentration of silicon nitride relative to the silicon dioxide powder in the slurry became 1 ppm to prepare a slurry for crushing and granulation. Using zirconia beads with an average particle diameter of 2.0 mm, the slurry for crushing and granulation was wet crushed until the BET specific surface area became 6.0 m 2 /g. Next, the slurry for crushing and granulation produced by the above method is spray-dried to obtain granulated powder. Regarding the obtained granulated powder, its average particle size was 80 μm and the moisture content was 1 wt%. The obtained granulated powder is melted by a hydrogen-oxygen flame to produce a slab-shaped opaque quartz glass ingot. Regarding the obtained slab-shaped opaque quartz glass ingot, the bubbles were uniformly dispersed when visually observed, and the appearance was also excellent.

(實施例7) 除了將氮化矽之添加量設為5 ppm以外,依據實施例1製造板塊狀不透明石英玻璃錠。 關於獲得之板塊狀不透明石英玻璃錠之氣泡,目視觀察時,均勻地分散,美觀方面亦優異。(Example 7) Except for setting the addition amount of silicon nitride to 5 ppm, a plate-shaped opaque quartz glass ingot was manufactured according to Example 1. Regarding the obtained slab-shaped opaque quartz glass ingot, the bubbles were uniformly dispersed when visually observed, and the appearance was also excellent.

(實施例8) 除了將氮化矽之添加量設為0.3 ppm以外,依據實施例1製造板塊狀不透明石英玻璃錠。表1示出製造條件。 關於獲得之板塊狀不透明石英玻璃錠之氣泡,藉由目視觀察,均勻地分散,美觀方面亦優異。(Example 8) Except for setting the addition amount of silicon nitride to 0.3 ppm, a plate-shaped opaque quartz glass ingot was manufactured according to Example 1. Table 1 shows the manufacturing conditions. The bubbles of the obtained slab-shaped opaque quartz glass ingot were uniformly dispersed by visual observation, and the appearance was also excellent.

(實施例9) 與實施例1同樣使作為二氧化矽原料粉末之非晶質二氧化矽分散於水中,將其濃度調整為50 wt%。其次,將獲得之漿料投入至珠磨機粉碎機,使用平均粒徑0.3 mm之氮化矽珠粒進行濕式粉碎,直至漿料中之氮化矽濃度成為1 ppm。其後,去除氮化矽珠粒,使用平均粒徑0.3 mm之氧化鋯珠粒對該漿料進行濕式粉碎,直至BET比表面積成為3.0 m2 /g。其次,對利用上述方法製作之漿料進行乾燥噴霧,獲得造粒粉。關於獲得之造粒粉,其平均粒徑為40 μm,含水率為1 wt%。利用氫氧焰使獲得之造粒粉熔融,製造板塊狀不透明石英玻璃錠。 關於獲得之不透明石英玻璃之氣泡,目視觀察時,均勻地分散,美觀方面亦優異。(Example 9) In the same manner as in Example 1, amorphous silica as the raw material powder of silica was dispersed in water, and the concentration was adjusted to 50 wt%. Next, put the obtained slurry into a bead mill and use silicon nitride beads with an average particle diameter of 0.3 mm to perform wet pulverization until the concentration of silicon nitride in the slurry becomes 1 ppm. Thereafter, the silicon nitride beads were removed, and the slurry was wet-pulverized using zirconia beads with an average particle diameter of 0.3 mm until the BET specific surface area became 3.0 m 2 /g. Next, the slurry prepared by the above method is dried and sprayed to obtain granulated powder. Regarding the obtained granulated powder, the average particle size was 40 μm and the moisture content was 1 wt%. The obtained granulated powder is melted by a hydrogen-oxygen flame to produce a plate-shaped opaque quartz glass ingot. Regarding the bubbles of the obtained opaque quartz glass, when visually observed, they were uniformly dispersed and were excellent in appearance.

(實施例10) 使與實施例1相同之作為二氧化矽原料粉末之非晶質二氧化矽分散於水中,將其濃度調整為70 wt%。其次,將經調整之漿料投入至珠磨機粉碎機,使用平均粒徑1.0 mm之氮化矽珠粒進行濕式粉碎,直至漿料中之氮化矽濃度成為1 ppm。其後,去除氮化矽珠粒,使用平均粒徑1.0 mm之氧化鋯珠粒對漿料進行濕式粉碎,直至BET比表面積成為8.0 m2 /g。其次,對漿料進行乾燥噴霧,獲得造粒粉。關於獲得之造粒粉,其平均粒徑為150 μm,含水率為1 wt%。利用氫氧焰使獲得之造粒粉熔融,製造板塊狀不透明石英玻璃錠。 關於獲得之板塊狀不透明石英玻璃錠之氣泡,目視觀察時,均勻地分散,美觀方面亦優異。(Example 10) The same amorphous silicon dioxide as the silicon dioxide raw material powder as in Example 1 was dispersed in water, and its concentration was adjusted to 70 wt%. Secondly, put the adjusted slurry into a bead mill and use silicon nitride beads with an average particle size of 1.0 mm for wet pulverization until the concentration of silicon nitride in the slurry becomes 1 ppm. After that, the silicon nitride beads were removed, and the slurry was wet pulverized using zirconia beads with an average particle diameter of 1.0 mm until the BET specific surface area became 8.0 m 2 /g. Next, the slurry is dried and sprayed to obtain granulated powder. Regarding the obtained granulated powder, its average particle size was 150 μm and the moisture content was 1 wt%. The obtained granulated powder is melted by a hydrogen-oxygen flame to produce a plate-shaped opaque quartz glass ingot. Regarding the obtained slab-shaped opaque quartz glass ingot, the bubbles were uniformly dispersed when visually observed, and the appearance was also excellent.

(實施例11) 使用非晶質二氧化矽(D10 :38 μm,D50 :67 μm,D90 :110 μm)作為二氧化矽原料粉末。使非晶質二氧化矽分散於水中,製成漿料,將濃度調整為67 wt%。其次,將經調整之漿料投入至珠磨機粉碎機中,使用平均粒徑1.0 mm之氮化矽珠粒進行濕式粉碎,直至氮化矽相對於漿料中之二氧化矽粉末之濃度成為500 ppm,製備漿料(A)。另一方面,利用不含發泡劑之二氧化矽原料粉末製備固形物濃度為67 wt%之漿料B。其後,利用漿料(B)以氮化矽相對於漿料中之二氧化矽粉末之濃度成為5 ppm之方式將漿料(A)加以稀釋,製備粉碎造粒用漿料。使用平均粒徑2.0 mm之石英珠粒對粉碎造粒用漿料進行濕式粉碎,直至BET比表面積成為6.0 m2 /g。 其次,對利用上述方法製作之粉碎造粒用漿料進行噴霧乾燥,獲得造粒粉。關於獲得之造粒粉,其平均粒徑為80 μm,含水率為1 wt%。利用氫氧焰使獲得之造粒粉熔融,製造柱狀不透明石英玻璃錠。 關於獲得之柱狀不透明石英玻璃錠之氣泡,目視觀察時,均勻地分散,美觀方面亦優異。(Example 11) Amorphous silicon dioxide (D 10 : 38 μm, D 50 : 67 μm, D 90 : 110 μm) was used as the silicon dioxide raw material powder. Disperse amorphous silicon dioxide in water to prepare a slurry, and adjust the concentration to 67 wt%. Secondly, put the adjusted slurry into the bead mill and use silicon nitride beads with an average particle size of 1.0 mm for wet pulverization until the concentration of silicon nitride relative to the silicon dioxide powder in the slurry It becomes 500 ppm, and a slurry (A) is prepared. On the other hand, slurry B with a solid content concentration of 67 wt% was prepared using silica raw material powder without foaming agent. After that, the slurry (A) was diluted with the slurry (B) so that the concentration of silicon nitride relative to the silica powder in the slurry became 5 ppm to prepare a slurry for crushing and granulation. Use quartz beads with an average particle size of 2.0 mm to wet pulverize the slurry for crushing and granulation until the BET specific surface area becomes 6.0 m 2 /g. Next, the slurry for crushing and granulation produced by the above method is spray-dried to obtain granulated powder. Regarding the obtained granulated powder, its average particle size was 80 μm and the moisture content was 1 wt%. The obtained granulated powder is melted by a hydrogen-oxygen flame to produce a columnar opaque quartz glass ingot. With regard to the bubbles of the obtained columnar opaque quartz glass ingot, when visually observed, the bubbles were uniformly dispersed, and the appearance was also excellent.

(比較例1) 使用平均粒徑150 μm之水晶粉作為二氧化矽原料粉末。又,使用平均粒徑2 μm之氮化矽作為發泡劑。將氮化矽相對於水晶粉之混合濃度設為0.2 wt%,將該混合粉末充分混合後,利用氫氧焰進行熔融,製造柱狀不透明石英玻璃錠。(Comparative example 1) Crystal powder with an average particle size of 150 μm is used as the raw material powder of silicon dioxide. In addition, silicon nitride with an average particle diameter of 2 μm was used as the blowing agent. The mixing concentration of silicon nitride with respect to the crystal powder is set to 0.2 wt%, and the mixed powder is thoroughly mixed, and then melted by a hydrogen-oxygen flame to produce a columnar opaque quartz glass ingot.

(比較例2) 使用與實施例1相同之非晶質二氧化矽作為二氧化矽原料粉末。使非晶質二氧化矽分散於水中,製成漿料,進行調整以使其濃度成為40 wt%。其次,將經調整之漿料投入至珠磨機粉碎機,使用平均粒徑3.5 mm之氮化矽珠粒進行濕式粉碎,直至氮化矽相對於漿料中之二氧化矽粉末之濃度成為20000 ppm,製備漿料A。藉由不含發泡劑之二氧化矽原料粉末製備固形物濃度為40 wt%之漿料B。其後,利用漿料B以氮化矽相對於漿料中之二氧化矽粉末之濃度成為0.5 ppm之方式將漿料A加以稀釋,製備粉碎造粒用漿料。使用平均粒徑3.5 mm之氧化鋯珠粒對粉碎造粒用漿料進行濕式粉碎,直至BET比表面積成為1.8 m2 /g。其次,對利用上述方法製作之粉碎造粒用漿料進行噴霧乾燥,獲得造粒粉。關於獲得之造粒粉,其平均粒徑為25 μm,含水率為4 wt%。利用氫氧焰使獲得之造粒粉熔融,製造柱狀不透明石英玻璃錠。 漿料之BET比表面積為1.8 m2 /g,較小,又,造粒粉之強度降低,造粒粉容易崩散,氫氧焰熔融時之良率降低。(Comparative Example 2) The same amorphous silicon dioxide as in Example 1 was used as the silicon dioxide raw material powder. Disperse amorphous silicon dioxide in water to prepare a slurry, and adjust the concentration to 40 wt%. Next, put the adjusted slurry into the bead mill and use silicon nitride beads with an average particle size of 3.5 mm to perform wet pulverization until the concentration of silicon nitride relative to the silicon dioxide powder in the slurry becomes 20000 ppm, slurry A was prepared. A slurry B with a solid concentration of 40 wt% was prepared from silica raw material powder without foaming agent. After that, the slurry A was diluted with the slurry B so that the concentration of silicon nitride relative to the silicon dioxide powder in the slurry became 0.5 ppm to prepare a slurry for crushing and granulation. Use zirconia beads with an average particle size of 3.5 mm to wet pulverize the slurry for crushing and granulation until the BET specific surface area becomes 1.8 m 2 /g. Next, the slurry for crushing and granulation produced by the above method is spray-dried to obtain granulated powder. Regarding the obtained granulated powder, its average particle size was 25 μm and the moisture content was 4 wt%. The obtained granulated powder is melted by a hydrogen-oxygen flame to produce a columnar opaque quartz glass ingot. The BET specific surface area of the slurry is 1.8 m 2 /g, which is small. In addition, the strength of the granulated powder is reduced, the granulated powder is easy to disintegrate, and the yield rate when the hydrogen-oxygen flame is melted is reduced.

(比較例3) 使用與實施例1相同之非晶質二氧化矽作為二氧化矽原料粉末。使非晶質二氧化矽分散於水中,將其濃度調整為40 wt%。其次,將經調整之漿料投入至珠磨機粉碎機中,使用平均粒徑3.5 mm之氮化矽珠粒進行濕式粉碎,直至漿料中之氮化矽濃度成為150 ppm。其後,去除氮化矽珠粒,使用平均粒徑3.5 mm之氧化鋯珠粒對添加有發泡劑之漿料進行濕式粉碎,直至BET比表面積成為1.8 m2 /g。其次,對利用上述方法製作之漿料進行乾燥噴霧,獲得造粒粉。關於獲得之造粒粉,其平均粒徑為250 μm,含水率為4 wt%。利用氫氧焰使獲得之造粒粉熔融,製造柱狀不透明石英玻璃錠。 漿料之BET比表面積為1.8 m2 /g,較小,造粒粉之強度降低,造粒粉容易崩散,氫氧焰熔融時之良率降低。(Comparative Example 3) The same amorphous silicon dioxide as in Example 1 was used as the silicon dioxide raw material powder. Disperse amorphous silica in water and adjust its concentration to 40 wt%. Secondly, put the adjusted slurry into a bead mill and use silicon nitride beads with an average particle size of 3.5 mm to perform wet pulverization until the silicon nitride concentration in the slurry becomes 150 ppm. After that, the silicon nitride beads were removed, and the zirconia beads with an average particle size of 3.5 mm were used to wet pulverize the slurry added with the foaming agent until the BET specific surface area became 1.8 m 2 /g. Next, the slurry prepared by the above method is dried and sprayed to obtain granulated powder. Regarding the obtained granulated powder, its average particle size was 250 μm and the moisture content was 4 wt%. The obtained granulated powder is melted by a hydrogen-oxygen flame to produce a columnar opaque quartz glass ingot. The BET specific surface area of the slurry is 1.8 m 2 /g, which is small, the strength of the granulated powder is reduced, the granulated powder is easy to collapse, and the yield rate of the hydrogen-oxygen flame is reduced.

(比較例4) 測定東曹石英公司製造之S等級之熔融透明玻璃之3點彎曲強度,結果為94.3 MPa。 [產業上之可利用性](Comparative Example 4) The 3-point flexural strength of the S grade fused transparent glass manufactured by Tosoh Quartz was measured and the result was 94.3 MPa. [Industrial availability]

本發明之不透明石英玻璃之熱線阻斷性、機械強度、表面平滑性優異,可適宜用於半導體製造裝置用構件、光學機器之零件等。又,根據本發明之不透明石英玻璃之製造方法,可穩定地製造熱線阻斷性、機械強度、表面平滑性優異之不透明石英玻璃。The opaque quartz glass of the present invention is excellent in heat ray blocking properties, mechanical strength, and surface smoothness, and can be suitably used for components for semiconductor manufacturing equipment, parts of optical equipment, and the like. In addition, according to the method for producing opaque quartz glass of the present invention, it is possible to stably produce opaque quartz glass having excellent heat-ray barrier properties, mechanical strength, and surface smoothness.

[表1]    漿料濃度(wt%) 氮化矽珠粒平均徑(mm) 氮化矽濃度 (ppm) 粉碎用 珠粒平均徑(mm) BET比表面積 (m2 /g) 造粒粉平均徑(μm) 水分含量(wt%) 製造錠形狀 實施例1 67 2.0 1 2.0 6 80 1 柱狀 實施例2 67 2.0 5 2.0 6 80 1 柱狀 實施例3 67 2.0 0.3 2.0 6 80 1 柱狀 實施例4 50 0.3 1 0.3 3 40 1 柱狀 實施例5 70 1.0 1 1.0 8 150 1 柱狀 實施例6 67 2.0 1 2.0 6 80 1 板塊狀 實施例7 67 2.0 5 2.0 6 80 1 板塊狀 實施例8 67 2.0 0.3 2.0 6 80 1 板塊狀 實施例9 50 0.3 1 0.3 3 40 1 板塊狀 實施例10 70 1.0 1 1.0 8 150 1 板塊狀 實施例11 67 1.0 5 2.0 6 80 1 柱狀 比較例1 - - 0.2 wt% - - - - - 比較例2 40 3.5 0.5 3.5 1.8 25 4 柱狀 比較例3 40 3.5 0.3 3.5 1.8 250 4 柱狀 [Table 1] Slurry concentration (wt%) Average diameter of silicon nitride beads (mm) Silicon nitride concentration (ppm) Average diameter of crushed beads (mm) BET specific surface area (m 2 /g) Average diameter of granulated powder (μm) Water content (wt%) Manufacturing ingot shape Example 1 67 2.0 1 2.0 6 80 1 Columnar Example 2 67 2.0 5 2.0 6 80 1 Columnar Example 3 67 2.0 0.3 2.0 6 80 1 Columnar Example 4 50 0.3 1 0.3 3 40 1 Columnar Example 5 70 1.0 1 1.0 8 150 1 Columnar Example 6 67 2.0 1 2.0 6 80 1 Plate Example 7 67 2.0 5 2.0 6 80 1 Plate Example 8 67 2.0 0.3 2.0 6 80 1 Plate Example 9 50 0.3 1 0.3 3 40 1 Plate Example 10 70 1.0 1 1.0 8 150 1 Plate Example 11 67 1.0 5 2.0 6 80 1 Columnar Comparative example 1 - - 0.2 wt% - - - - - Comparative example 2 40 3.5 0.5 3.5 1.8 25 4 Columnar Comparative example 3 40 3.5 0.3 3.5 1.8 250 4 Columnar

[表2]    平均氣泡徑(μm) 氣泡形狀 氣泡正圓度 密度 (g/cm3 反射率 (%) 白度 (%) 3點彎曲強度(MPa) 燒製完成面之表面粗糙度(μm) Ra(μm) Rmax 實施例1 10 獨立球狀 0.95 2.19 86 95 93 0.4 0.7 實施例2 18 獨立球狀 0.92 2.15 81 90 90 0.5 0.7 實施例3 2 獨立球狀 0.98 2.20 88 98 94 0.3 0.5 實施例4 10 獨立球狀 0.95 2.19 86 95 93 0.4 0.6 實施例5 10 獨立球狀 0.95 2.19 86 95 93 0.4 0.6 實施例6 25 獨立球狀 0.92 2.19 82 84 84 0.6 0.8 實施例7 28 獨立球狀 0.92 2.15 80 80 80 0.6 0.8 實施例8 15 獨立球狀 0.93 2.20 83 92 90 0.5 0.7 實施例9 25 獨立球狀 0.92 2.19 82 84 85 0.6 0.8 實施例10 25 獨立球狀 0.91 2.19 82 84 85 0.6 0.8 實施例11 10 獨立球狀 0.95 2.15 87 96 93 0.4 0.6 比較例1 80 獨立球狀 0.90 2.10 40 50 67 3.0 7.0 比較例2 1 獨立球狀 0.98 2.21 70 70 77 0.3 0.5 比較例3 100 結合 0.80 1.17 70 70 30 50 80 [Table 2] Average bubble diameter (μm) Bubble shape Bubble roundness Density (g/cm 3 ) Reflectivity(%) BaiDu(%) 3-point bending strength (MPa) Surface roughness of fired surface (μm) Ra (μm) Rmax Example 1 10 Independent spherical 0.95 2.19 86 95 93 0.4 0.7 Example 2 18 Independent spherical 0.92 2.15 81 90 90 0.5 0.7 Example 3 2 Independent spherical 0.98 2.20 88 98 94 0.3 0.5 Example 4 10 Independent spherical 0.95 2.19 86 95 93 0.4 0.6 Example 5 10 Independent spherical 0.95 2.19 86 95 93 0.4 0.6 Example 6 25 Independent spherical 0.92 2.19 82 84 84 0.6 0.8 Example 7 28 Independent spherical 0.92 2.15 80 80 80 0.6 0.8 Example 8 15 Independent spherical 0.93 2.20 83 92 90 0.5 0.7 Example 9 25 Independent spherical 0.92 2.19 82 84 85 0.6 0.8 Example 10 25 Independent spherical 0.91 2.19 82 84 85 0.6 0.8 Example 11 10 Independent spherical 0.95 2.15 87 96 93 0.4 0.6 Comparative example 1 80 Independent spherical 0.90 2.10 40 50 67 3.0 7.0 Comparative example 2 1 Independent spherical 0.98 2.21 70 70 77 0.3 0.5 Comparative example 3 100 Combine 0.80 1.17 70 70 30 50 80

no

no

Claims (12)

一種不透明石英玻璃,其氣泡之形狀為獨立球狀,平均粒徑為2~30 μm,平均正圓度為0.8以上,上述不透明石英玻璃之密度為1.90~2.20 g/cm3 ,白度為80以上及/或於厚度3 mm之波長0.2~3 μm之光之反射率為80%以上; 再者,白度為使用色彩色差計依據JIS Z 8722測定之亮度; 關於氣泡之平均粒徑,對試樣進行切割,藉由桌上型掃描式電子顯微鏡觀察20個以上氣泡之形狀,對其圖像進行處理,測定各氣泡之面積A,代入下述式1求出值D,將該值D之平均值設為平均粒徑; 關於氣泡之平均正圓度,對試樣進行切割,藉由桌上型掃描式電子顯微鏡觀察20個以上氣泡之形狀,對其圖像進行處理,測定各氣泡之面積A及外周L,代入下述式2求出值S,將該值S之平均值設為平均正圓度;
Figure 03_image003
π為圓周率。
An opaque quartz glass, the bubble shape is independent spherical, the average particle size is 2-30 μm, the average roundness is 0.8 or more, the density of the above-mentioned opaque quartz glass is 1.90-2.20 g/cm 3 , and the whiteness is 80 The above and/or the reflectance of light with a thickness of 3 mm and a wavelength of 0.2~3 μm is above 80%; In addition, the whiteness is the brightness measured with a color difference meter in accordance with JIS Z 8722; Regarding the average particle size of the bubbles, The sample is cut, the shape of more than 20 bubbles is observed with a desktop scanning electron microscope, the image is processed, the area A of each bubble is measured, and the value D is obtained by substituting the following formula 1 into the value D The average value is set as the average particle size; Regarding the average roundness of the bubbles, cut the sample, observe the shape of more than 20 bubbles with a desktop scanning electron microscope, process the image, and measure each bubble The area A and outer circumference L of, substitute the following formula 2 to obtain the value S, and set the average value of the value S as the average roundness;
Figure 03_image003
π is the circle ratio.
如請求項1之不透明石英玻璃,其3點彎曲強度為80 MPa以上。For example, the opaque quartz glass of claim 1, its 3-point bending strength is 80 MPa or more. 如請求項1或2之不透明石英玻璃,其燒製完成面之表面粗糙度Ra為0.7 μm以下。For the opaque quartz glass of claim 1 or 2, the surface roughness Ra of the fired surface is less than 0.7 μm. 一種不透明石英玻璃之製造方法,其係向二氧化矽粉末中添加發泡劑並進行加熱熔融之不透明石英玻璃之製造方法,其特徵在於,對使二氧化矽粉末以45~75 wt%分散於水中而成之漿料,使用平均粒徑0.1 mm~3 mm之氮化矽珠粒作為粉碎介質進行濕式粉碎,將由氮化矽珠粒之磨耗所產生之氮化矽粉末作為發泡劑進行加熱熔融。An opaque quartz glass manufacturing method, which is a method of manufacturing opaque quartz glass in which a foaming agent is added to silicon dioxide powder and heated and melted, characterized in that the silicon dioxide powder is dispersed in 45-75 wt% A slurry made in water, using silicon nitride beads with an average particle size of 0.1 mm to 3 mm as the grinding medium for wet grinding, and silicon nitride powder produced by the abrasion of the silicon nitride beads as a blowing agent Heat to melt. 如請求項4之不透明石英玻璃之製造方法,其中,對二氧化矽粉末之粉碎時間進行調整,將發泡劑之添加量調整為0.1~100 ppm,使用除氮化矽珠粒以外之平均粒徑0.1~3 mm之1種或複數種珠粒進一步進行濕式粉碎,使漿料中所含之固形物之BET比表面積為2 m2 /g以上,對將漿料進行噴霧乾燥造粒所得之平均粒徑為30~200 μm、含水率為3 wt%以下之球形造粒粉進行加熱熔融。Such as the manufacturing method of opaque quartz glass of claim 4, in which the crushing time of the silicon dioxide powder is adjusted, the addition amount of the blowing agent is adjusted to 0.1-100 ppm, and the average particles other than the silicon nitride beads are used One or more kinds of beads with a diameter of 0.1~3 mm are further wet crushed to make the BET specific surface area of the solids contained in the slurry 2 m 2 /g or more, and the slurry is spray-dried and granulated The spherical granulated powder with an average particle size of 30-200 μm and a moisture content of 3 wt% or less is heated and melted. 如請求項4之不透明石英玻璃之製造方法,其中,對發泡劑相對於二氧化矽粉末之添加比率設為200~10000 ppm之漿料進行稀釋,將發泡劑相對於二氧化矽粉末之添加比率調整為0.1~500 ppm,加入除氮化矽珠粒以外之平均粒徑0.1 mm~3 mm之粉碎用珠粒進行濕式粉碎,使漿料中所含之固形物之BET比表面積為2 m2 /g以上,對將漿料進行噴霧乾燥造粒而製成實質上為球形之平均粒徑為30~200 μm、含水率為3 wt%以下之造粒粉進行加熱熔融。For example, the manufacturing method of opaque quartz glass of claim 4, wherein the slurry whose addition ratio of the blowing agent to the silica powder is set to 200~10000 ppm is diluted, and the blowing agent is relative to the silica powder. The addition ratio is adjusted to 0.1~500 ppm, and pulverizing beads with an average particle size of 0.1 mm~3 mm other than the silicon nitride beads are added for wet pulverization, so that the BET specific surface area of the solids contained in the slurry is 2 m 2 /g or more, the slurry is spray-dried and granulated to form a substantially spherical granulated powder with an average particle diameter of 30-200 μm and a moisture content of 3 wt% or less by heating and melting. 如請求項5之不透明石英玻璃之製造方法,其中,濕式粉碎之方法為珠磨機粉碎、球磨機粉碎、振動磨機粉碎、磨碎機(attritor)粉碎之1種或2種以上之組合。For example, the method for manufacturing opaque quartz glass in claim 5, wherein the wet pulverization method is one or a combination of bead mill pulverization, ball mill pulverization, vibration mill pulverization, and attritor pulverization. 如請求項6之不透明石英玻璃之製造方法,其中,濕式粉碎之方法為珠磨機粉碎、球磨機粉碎、振動磨機粉碎、磨碎機粉碎之1種或2種以上之組合。For example, the method for manufacturing opaque quartz glass of claim 6, wherein the wet pulverization method is one or a combination of bead mill pulverization, ball mill pulverization, vibration mill pulverization, and grinder pulverization. 6、7、8中任一項之不透明石英玻璃之製造方法,其利用氫氧焰對熔融原料進行加熱熔融。The manufacturing method of opaque quartz glass in any one of 6, 7, and 8, which uses a hydrogen-oxygen flame to heat and melt the molten raw material. 6、7、8中任一項之不透明石英玻璃之製造方法,其在真空環境下對熔融原料進行加熱熔融。The manufacturing method of opaque quartz glass in any one of 6, 7, and 8, which heats and melts the molten raw material in a vacuum environment. 一種不透明石英玻璃,其係藉由請求項9之方法製造者,其OH基濃度為100~1000 ppm。An opaque quartz glass manufactured by the method of claim 9 with an OH group concentration of 100-1000 ppm. 一種不透明石英玻璃,其係藉由請求項10之方法製造者,其OH基濃度為10 ppm以下。An opaque quartz glass manufactured by the method of claim 10, the OH group concentration of which is 10 ppm or less.
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